|Publication number||US4261942 A|
|Application number||US 06/088,587|
|Publication date||Apr 14, 1981|
|Filing date||Oct 26, 1979|
|Priority date||Oct 30, 1978|
|Publication number||06088587, 088587, US 4261942 A, US 4261942A, US-A-4261942, US4261942 A, US4261942A|
|Inventors||Tadao Shimamura, Yasufumi Seo|
|Original Assignee||Shikoku Kasei Kogyo Co., Ltd.|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (3), Referenced by (3), Classifications (10)|
|External Links: USPTO, USPTO Assignment, Espacenet|
1. Field of the Invention
The present invention relates to the production of tablets of sodium dichloroisocyanurate, and more particularly to the production of tablets having flame resistance and thermal stability sufficient to avoid chain reaction thermal decomposition.
Sodium dichloroisocyanurate is a widely used solid chlorine compound which is effective to release active chlorine for various purposes such as for sterilizing water in swimming pools and sewerage.
2. Description of the Prior Art
For storing, transportation and use, it is preferable to supply sodium dichloroisocyanurate in tablet form.
Production of sodium dichloroisocyanurate in tablet form is disclosed in Japanese Pat. No. 513,484 (Jap. Pat. Publn. No. 23 198/1967) granted to the assignee of the present patent application. In the referenced patent, sodium dichloroisocyanurate powder is kneaded with sufficient water to produce a predetermined water content in the resulting kneaded material. The kneaded material is compressed into tablets using a surface pressure of about 1,000 Kg/cm3. U.S. Pat. No. 3,956,444 to William H. Kibbel, Jr. discloses sodium dichloroisocyanurate dihydrate tablets produced by a surface pressure of from about 2,000 to about 10,000 p.s.i.
The method disclosed in the Japanese patent has the disadvantage that wet dichloroisocyanurate is sticky. The stickiness adversely affects continuously supplying fixed amounts of the material to a tabletting machine. Therefore, this method is not suitable for use on an industrial scale.
The method of the United States patent has the advantage that tablets of sodium dichloroisocyanurate dihydrate produced thereby have flame resistance to avoid chain reaction thermal decomposition, but it has the disadvantage that, due to a water content of 14.1 weight %, it is sticky. The stickiness causes the same operational difficulty as in the Japanese patent. There is also the possibility that water may be released with a slight increase in heat in the tablet. Since the temperature at which the dihydrate is converted to the monohydrate lies at about 66.7° C., the resulting tablet products may be thus converted during storage and/or transportation and may cause agglomeration due to adhesion thereof.
Accordingly, a principal object of the present invention is to provide a method of producing tablets of sodium dichloroisocyanurate which can obviate and overcome the disadvantages involved in the prior art methods.
A specific object of the invention is to provide a method of producing tablets of sodium dichloroisocyanurate, which method can be easily and safely carried out on an industrial scale to make tablets having flame resistance, no thermal decomposition, and stability during storage and transportation without generating gas or caking.
Hitherto, it was known that sodium dichloroisocyanurate containing 11 weight % or more moisture has flame resistance and does not cause chain reaction decomposition. Anhydrous or hydrous sodium dichloroisocyanurate in the form of powder and granules containing 11 weight % or less moisture causes chain reaction combustion including a flame.
However, it has been discovered by the applicants that tablets obtained by tabletting sodium dichloroisocyanurate which was previously made into granules containing 7 to 11 weight % moisture have desirable flame resistance, do not cause thermal decomposition and have high stability during storage and transportation.
According to the present invention, therefore, the said and other objects are attained by producing tablets of sodium dichloroisocyanurate by tabletting granular sodium dichloroisocyanurate with moisture of 7 to 11 weight %.
It is preferable that the granules have a bulk density of 0.9 g/cm3 or more. Such granules can be prepared by extruding wet sodium dichloroisocyanurate obtained in the manufacturing process through a screen with a large number of openings to form columnar pellets, passing the pellets through a fluidized bed heating chamber to dry the same until they contain substantially no free water and have a moisture content in the range of 7 to 11 weight %, compacting the dried pellets to bulk density of at least 0.8 g/cm3, crushing the compacted pellets, then tabletting the granules under moderate pressure.
Moisture adjusted hot air can be fed to the fluidized heating chamber to obtain the pellets with a moisture content in the desired level. The monohydrate (having a moisture content of 7.6%) and the dihydrate (having a moisture content of 14.06%) have different vapor pressures at different temperatures. Thus, by adjusting the humidity and temperature of the hot air in the fluidized bed heating chamber, to balance the vapor pressure with that of the desired material emerging from the operation, either monohydrate or the dihydrate may be selectively obtained.
Furthermore, by appropriate temperature, humidity and residence time control, a mixture of monohydrate and dihydrate may be obtained.
The compacting and crushing steps may be carried out using a conventional roll type compactor and a conventional impeller type crusher, respectively. The resulting granules have a moisture content of 7 to 11 weight %, are not sticky and thus can be quite smoothly supplied to a tabletting machine in a fixed amount in each supply by simply charging the granules into a hopper of the tabletting machine without using an auxiliary feeding mechanism. The tabletting machine may be of any conventional type. The smooth supply of the granules in fixed amounts for each charging operation into the tabletting machine decreases the irregularity in amount for each tablet and helps bleed air from the gaps between neighboring granules during the tabletting operation. Such air gaps produce a so-called "capping phenomenon". Avoidance of such air gaps permits a hard tablet to be obtained at relatively low tabletting pressures. Further, the resulting tablets do not release free water to cause caking thereof, are easily handled and packaged, and they decrease the loss of active chlorine during storage. The tablets obtained by the method according to the present invention have a high effective chlorine content of 57 to 60%, compared to a chlorine content in sodium dichloroisocyanurate dihydrate of 55.4%.
The single drawing shows a schematic illustration of an apparatus suitable for carrying out the method according to the present invention.
Wet or moisture containing sodium dichloroisocyanurate for use in the present invention can be obtained using any suitable conventional manufacturing process. For instance, it can be produced by neutralizing dichloroisocyanuric acid with sodium hydroxide or reacting three components of trichloroisocyanurate, cyanuric acid and sodium hydroxide in a molar ratio of 2:1:3 in water, and then concentrating under reduced pressure or cooling the reaction mixture to separate and gather the resulting wet cake.
Referring now to the FIGURE, the wet raw material is contained in a raw material tank 1 having a screw feeder 10 and is extruded through a screen extruder type granulator 2 to form thin rods. Columnar pellets are formed from the rods by the breaking thereof from their own weight. The columnar pellets are dried in a fluidized bed type dryer 3. Fluidized bed type dryer 3 includes a drying chamber 11 which includes a first area 12 and a second area 13 separated by a divider 14. A blower 15 blows air through a moisture conditioning and heating element 16 into a region 17 below screen 18 of first area 12.
Similarly, a blower 19 provides air through a moisture conditioning and heating element 20 to a region 21 below a screen 22.
The columnar pellets breaking off from granulator 2 fall into first area 12 where they are supported by the air flowing thereinto through screen 18 and are dried as they move toward divider 14. The columnar pellets continue through second area 13 where they are further dried and/or moisture conditioned by air flowing through screen 22. During drying in dryer 3, the rods or pellets are broken into relatively short columnar pellets of substantially uniform size or length. At least the free water adhered to and contained in the pellets is removed and the total water content thereof is in the desired range.
Waste air from drying chamber 11 is exhausted through a cyclone-type separator 23 for removing dust and fine particles from the waste air.
The dried pellets pass from second area 13 into a vertical conveyor 4 which raises them to a screw-type conveyor 26 feeding a conventional roll type compactor 5 having a pair of rotary rolls 24 and 25. At least one of the rotary rolls 24 and 25 has a rough surface which is effective to compact the dried pellets with the aid of the other roll. The resulting compact pellets are crushed by a rotary impeller 6 to produce granules. The granules are fed to a vibrating screen 7 for dressing thereof and are then supplied to a tabletting machine 8 where the desired tablets are produced.
The diameter of each opening in the screen (not shown) of the screen extruder type granulator 2 is preferably from about 0.5 to about 3.0 mm and most preferably from about 1.5 to about 2.0 mm.
Moisture adjusted hot air containing about 26 g of water to 1 Nm3 of dry air at a temperature of from about 50° to about 100° C. is supplied to the fluidized bed type dryer 3.
The water or moisture content of the wet sodium dichloroisocyanurate fed to the screen extruder type granulator 2 is regulated to a value of from about 15 to about 30%. A water content lower than 15% makes granulation difficult to accomplish. In addition, an observable powdering phenomenon appears during subsequent drying steps. A water content exceeding 30% permits the thin rod-like pellets formed by the granulator 2 to adhere to one another to form agglomerates in the drying step to make it impossible to uniformly dry them thus interfering with smooth and continuous operation.
The rotational frequency of the rolls 24 and 25 of the roll type compactor 5 is preferably set at a low level, such as, for example, 5 to 50 rpm. The pressure between the rolls of the roll type compactor 5 is preferably in a range of 500 to 1,500 Kg of force per linear centimeter of contact line between rolls 24 and 25.
The granules from the vibrating screen 7 have a size distribution in a range of 10 to 60 mesh, of which the main part lies in a range of 14 to 28 mesh. The average bulk density lies in a range of 0.8 to 1.2 g/cm3. Excessively fine or coarse particles which pass vibrating screen 7 are recovered in a receiver 27.
Powdered or fine granules of sodium dichloroisocyanurate recovered from cyclone-type separator 23 and from receiver 27 may be recycling into raw material tank 1 by adding a predetermined amount of water or fresh raw material thereto to regulate the water content therein in preparation for again passing this material through the screen extruder type granulator 2.
Tabletting pressure in tabletting machine 8 is preferably at least 350 Kg/cm2 and more preferably from about 350 to about 750 Kg/cm2 to impart flame resistance to the product. Higher pressure values are not always necessary for the tabletting operation. If necessary, a small amount of a lubricant such as a metal salt of stearic acid may be mixed to the granules prior to supplying them to the tabletting machine.
The tablets obtained by the method according to the invention in which no lubricant is used have a bulk density of 1.3 to 1.5 g/cm3, contain 7 to 11 weight % moisture and have good solubility in water.
The method according to the invention ensures safety during the operation. The chemically unstable wet sodium dichloroisocyanurate is first extruded through the screen extruder type granulator 2 under a low loading pressure. The resulting pellets are dried to a chemically stable state in which they contain substantially no free water. The dried pellets are compacted in roll type compactor 5 under high loading pressure. The resulting compacted granules are crushed in rotary impeller 6 and then are tabletted in tabletting machine 8 to obtain the final product.
Powdery solids of dichloroisocyanurate containing 25.0% moisture and stored in a raw material tank 1 were continuously fed by a screw feeder at a rate of 200 Kg/hr to a screen extruder type granulator 2 with a screen having a large number of openings, each of which had a diameter of 1.5 mm to extrude therefrom the raw material to form thin rods which broke off of their own weight to form columnar pellets which fell into first area 12 of drying chamber of a fluidized bed type dryer 3. Fluidized bed type dryer 3 had a surface area of 0.75 m2 and air heated in a temperature range of from about 75° to about 85° C. and containing 25.9 g of moisture to 1 Nm3 of dry air was continuously supplied. The pellets passed through the dryer chamber over an average residence time of 20 minutes to form pellets of sodium dichloroisocyanurate hydrate containing 10.0% moisture.
The resulting pellets were compacted in a roll type compactor 5, crushed by a rotary impeller 6 and then sieved by a vibrating screen 7 to recover granules of 60 or below in mesh-size. The resulting granules had an average bulk density of 0.93 g/cm3.
The granules were fed to a tabletting machine 8 to continuously prepare tablets at a surface pressure of 500 Kg/cm2. The tablets had an average weight of 15 g. The operation was continued for 12 hours and 1,300 Kg of produce was produced.
The tablets produced had an average bulk density of 1.45 g/cm3 and showed good flame resistance. The weight deviation of the product was ±2.0%.
As a comparative example, sodium dichloroisocyanurate powder containing 10.0% moisture was fed to the tabletting machine without performing the other steps of the process. The supply of raw material became unstable and the capping phenomenon occurred which required slowing the tabletting operation. The yield of product for 12 hours operation was limited to 940 Kg. The weight deviation of the product was ±5.0%.
Grooves 10 mm in depth, 20 mm in width and 100 mm in length were cut in porous fire-brick. One set of grooves was packed to a density of about 1.0 g/cm3 with granular sodium dichloroisocyanurate containing various amounts of moisture. Another set of grooves was packed to about 0.7 g/cm3 with powdered sodium dichloroisocyanurate containing various amounts of moisture. A hot nichrome wire was applied to one end of each filled groove to attempt to cause chain-reaction thermal decomposition. The time required for transmitting thermal decomposition a distance of 50 mm was measured for each case. The results are shown in Table 1.
TABLE 1______________________________________Moisture content Transmission velocity (sec)of samples Granular form Powder form______________________________________1.6 83 --2.8 -- 2335.0 123 --7.0 255 --9.5 -- 32510.0 naturally extin- 350 guished after 25 mm10.5 no transmission 41211.0 " naturally extin- guished after 30 mm11.5 " no transmission______________________________________
The results show that chain-reaction thermal decomposition occurs when the moisture content is less than 10% and 11% for granular and powdered sodium dichloroisocyanurate, respectively.
Tablets of sodium dichloroisocyanurate were prepared in accordance with the method as described in Example 1 having different moisture contents and tabletting pressures. Each tablet was placed on a nichrome wire having a length of 200 mm and electric resistance of 0.8Ω arranged on porous fire-brick. The relation between the moisture content of each tablet and the transmission time of thermal decomposition thereof was measured. The results are shown in Table 2.
TABLE 2______________________________________Moisture Tabletting at surface pressure ofcontent 350 Kg/cm2 750 Kg/cm2______________________________________1.6 Completely decomposed Completely decomposed in 120 sec. in 134 sec.5.0 Completely decomposed Completely decomposed in 178 sec. in 210 sec.7.0 Naturally extinguished Naturally extinguished after some transmis- after some transmis- sion sion7.6 No decomposition No decomposition10.0 " "11.0 " "13.5 " "______________________________________
The results show that the thermal stability of sodium dichloroisocyanurate in tablet form is far better than that in the form of granule or powder and that the sodium dichloroisocyanurate tablets containing moisture of more than 7.0 do not support chain-reaction thermal decomposition.
A number of sodium dichloroisocyanurate tablets containing different percentages of moisture were prepared in accordance with the method as described in Example 1 using tabletting surface pressure of 500 Kg/cm2. The different moisture contents were produced by varying the residence time of the tablets in the fluidized bed type dryer 3. Twenty tablets of each kind, each tablet having a weight of 15 g, were sealed in glass bottles of 300 ml and stored in a constant temperature chamber maintained at 30° C. The amount of generated decomposed gas was measured by the change in height of a column of a saturated aqueous solution of sodium chloride which was communicated to the sealed bottle. Caking of the pellets was noted by visual observation. The results are shown in Table 3.
TABLE 3______________________________________ Amount of decomposed gas (height of column in mm)Moisture content After 30 days After 60 days State of caking______________________________________1.6 15 17 none5.0 10 12 "7.6 14 20 "10.0 25 40 "11.0 50 96 slight13.5 896 1290 apparent14.1 1770 3246 "______________________________________
The results show that generation of decomposed gas becomes marked when the moisture content of the tablets exceeds 11% and especially when the moisture content of the tablets exceeds 14.1%. The tablets may release more or less free water accompanying vigorous generation of decomposed gas. An observable caking phenomenon appears when the moisture content of the tablets exceeds 11%.
Sodium dichloroisocyanurate tablets were prepared in accordance with the method as described in Example 1, having different moisture contents and tabletting surface pressure. The moisture content was controlled by varying the residence time of the tablets in the fluidized bed type dryer 3. Each kind of tablet was placed in a constant temperature chamber maintained at 30° C. and at a humidity of 72%. Dissolubility of the tablets was checked to obtain the results shown in Table 4.
The dissolubility was determined by placing each tablet having a weight of 15 g on a wire-netting with 1/2 inch stitches, submerging it in stirred water at 20° C., and measuring the time required for it to become completely dissolved in the water.
TABLE 4______________________________________ Time for dissolution (sec) Stand Stand Tabletting for 24 for 48Moisture pressure Just after hours after hours aftercontent (%) (Kg/cm2) tabletting tabletted tabletted______________________________________ 350 185 300 420 500 200 350 5006.0 750 260 480 530 1000 300 520 550 350 330 290 350 500 325 330 38010.0 750 320 330 390 1000 320 350 420 350 35 250 380 500 75 260 41013.0 750 135 340 430 1000 420 310 530______________________________________
The tablets containing more than 11% moisture were observed to shrink when stored in humid conditions. Tablets containing less than 10% moisture were observed to expand under the same humid conditions. Tablets containing 13 and 6% moisture have a high variation in dissolubility depending on the elapsed time after tabletting. Tablets containing 10% show substantially constant dissolubility over time.
Having described specific embodiments of the invention with respect to the accompanying drawings, it is to be understood that the invention is not limited to those precise embodiments, and that various changes and modifications may be effected therein by one skilled in the art without departing from the scope or spirit of the invention as defined in the appended claims.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US3886249 *||Mar 19, 1973||May 27, 1975||Fmc Corp||Production of granular sodium dichloroisocyanurate|
|US4024257 *||Apr 24, 1975||May 17, 1977||Fmc Corporation||Rapidly-soluble sodium dichloroisocyanurate dihydrate tablet|
|US4082532 *||Apr 19, 1977||Apr 4, 1978||S.A.F. Societe Agricole Et Fonciere S.A.||Process for making extruded cattle manure pellets|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US4394336 *||Jul 20, 1981||Jul 19, 1983||Shikoku Kasei Kogyo Company Ltd.||Production of tablets of sodium dichloroisocyanurate|
|US5114647 *||Feb 1, 1991||May 19, 1992||Olin Corporation||Effervescent tablets having increased disintegration rates|
|EP0313527A2 *||Oct 20, 1988||Apr 26, 1989||CASTELLINI S.p.A.||A method for continuous sterilization of the waste pipelines of medical equipment or accessories, and a relative preparation|
|U.S. Classification||264/118, 264/141|
|International Classification||A01N43/64, A01N59/00, C02F1/76, A61K9/20|
|Cooperative Classification||A01N59/00, C02F1/76|
|European Classification||C02F1/76, A01N59/00|